Corrosion Inhibitors – Boiler Systems

(Amines & Oxygen Scavengers)

Boiler systems can be very complex, and an intimate knowledge of the system’s purpose and components is a prerequisite to properly treating a given system. They must be treated with a comprehensive approach beginning with the preboiler section, then the boiler, followed by the condensate system. Corrosion can lead to pitting and metal loss that can cause critical system failures – sometimes catastrophic. It is estimated that corrosion in boiler systems cost the industry billions of dollars every year.

Oxygen Scavengers

Corrosion is most commonly caused by dissolved gases (primarily oxygen and carbon dioxide), low pH, the attack of mechanically stressed areas, and under-deposit attack. To avoid the corrosion of vital (and costly) metal components throughout boiler systems, external treatment of the feedwater is performed in order to remove dissolved oxygen (DO) and other contaminants such as iron and copper. The majority of the DO removal, along with other dissolved gases, is done by mechanical deaeration. In order to remove the remaining oxygen and provide the boiler with high-purity feedwater, the application of an oxygen scavenger is utilized. Additionally, applying chemical oxygen scavengers indirectly leads to passivated metal surfaces and lower amounts of metal oxide that is transported to the boiler. Multiple factors such as system design, pressure and temperature, and the quality of the make-up water play a key role in determining the proper O2 scavenger to be applied (Non-volatile, Volatile, Organic or Inorganic).

DEHA (Diethylhydroxylamine)
Hydrazine (35%)
Erythorbic Acid (Solid)

Neutralizing and Filming Amines

Due to the complexity of steam generating boiler equipment and design, a systematic holistic approach must be utilized to effectively treat each system, and its individual components. Corrosion control begins by effectively removing contaminants in the feedwater, and then by controlling deposition within the boiler. The final phase of boiler system corrosion control occurs in the Condensate System. Because of carryover, iron and copper corrosion is not limited to the piping and equipment of the condensate system. Corrosion products and process chemicals can return to the boiler causing damaging boiler deposits, and deposits on steam-driven equipment. If this happens, the boiler’s system performance is reduced and operational, maintenance and repair costs are increased.

From the reaction between heat, water, and sodium carbonate and bicarbonate, carbon dioxide (CO2) is liberated in the generated steam; and is distributed throughout the entire system. As the steam is used and then condensed, the CO2 dissolves in water and drives down the pH, resulting in the formation of carbonic acid (H2CO3). The resultant carbonic acid formation further lowers pH, and will corrode condensate piping and equipment. In order to prevent acid attack corrosion, and to maintain proper pH, neutralizing amines such as morpholine and cyclohexylamine are used. When added to water, neutralizing amines hydrolyze and generate the required hydroxide ions for neutralization.

Cyclohexylamine
Morpholine
DEAE (Diethylaminoethanol) / DEEA (Diethylethanolamine)
DEHA (Diethylhydroxylamine)